2022
DOI: 10.1016/j.isci.2022.104011
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Electrochemical CO2 reduction - The macroscopic world of electrode design, reactor concepts & economic aspects

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Cited by 61 publications
(56 citation statements)
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“…In addition, the removal of the liquid electrolyte eliminates GDE flooding and reduces the possibility of electrocatalyst deactivation by the deposition of electrolyte impurities. 156 However, there are also some shortcomings for this kind of configuration. First, the reaction environment is difficult to adjust because of the absence of a catholyte.…”
Section: Electrolyzer Designmentioning
confidence: 99%
“…In addition, the removal of the liquid electrolyte eliminates GDE flooding and reduces the possibility of electrocatalyst deactivation by the deposition of electrolyte impurities. 156 However, there are also some shortcomings for this kind of configuration. First, the reaction environment is difficult to adjust because of the absence of a catholyte.…”
Section: Electrolyzer Designmentioning
confidence: 99%
“…9,10 The use of gas diffusion electrodes (GDEs) is one approach to overcome this problem originating from the low solubility and slow diffusion in the substrate. [11][12][13][14][15][16][17][18][19][20][21][22][23][24][25][26][27] Gaseous substrates can be directly supplied to the triple-phase boundary at the GDE, where the catalyst material, electrolyte, and gas pores intersect. 10,28 For example, de Arquer et al achieved a current density of 1.3 A/cm 2 for ethylene formation at 45% energy efficiency using a GDE loaded with Cu nanoparticles, 29 and de Jesus and his coworkers achieved 600 mA/cm 2 for CO formation at a faradaic efficiency (FE) of 80% using a gas-fed zero-gap electrolyzer loaded with Ag nanocubes.…”
Section: Introductionmentioning
confidence: 99%
“…While the catalyst is key to facilitate the catalytic conversion of CO 2 , the electrode assembly and reactor setup play an equally important role to achieve efficient CO 2 reduction reaction (CO 2 RR) processes of industrial relevance. Along this line, a minimum current density of 200 mA cm −2 with Faraday efficiencies (FEs) of at least 60% for multicarbon products are required [2][3][4][5]. Herein, utilization of gas diffusion electrodes (GDEs) in continuously driven flow cells showed promising results toward this aim.…”
Section: Introductionmentioning
confidence: 99%